Renaud Escudié
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Renaud Escudié has a total of 211 co-authors. Here are the top co-authors by number of shared publications:
- Jean-Philippe Steyer
INRAE, Univ Montpellier, LBE, Narbonne, France
36 shared publications - Nicolas Bernet
INRAE, University of Montpellier, LBE, 102 Avenue des Etangs, 11100 Narbonne, France
35 shared publications - Eric Trably
Institut National de Recherche pour l'Agriculture, l'Alimentation et l'Environnement (INRAE), University of Montpellier, LBE, 102 Avenue des Etangs, Narbonne 11100, France
32 shared publications Jean-Philippe Delgenès
INRAE, Univ Montpellier, LBE, 102 avenue des Etangs, 11100, Narbonne, France
15 shared publications- Giovanni Esposito
Department of Civil, Architectural and Environmental Engineering, University of Naples Federico II, via Claudio 21, 80125 Naples, Italy
11 shared publications - Gabriel Capson-Tojo
INRAE, Univ. Montpellier, LBE 102 avenue des étangs, 11100 Narbonne, France
10 shared publications
Latest Publications
- Open Access
- 27 October 2026
- Published by Elsevier in Bioresource Technology
- Vol. 465
A hydrogen-adapted microbial community enhances in situ biomethanation robustness under increasing organic loading rate
- 27 October 2026
- Published by Elsevier in Bioresource Technology
- Vol. 465
Open AccessA hydrogen-adapted microbial community enhances in situ biomethanation robustness under increasing organic loading rate
- Open Access
- 28 April 2026
- Published by Elsevier in New Biotechnology
- Vol. 93, 351-361
Substrate biochemical composition does not impact hydrogen consumption rate but metabolite production during batch in-situ biomethanation process
- 28 April 2026
- Published by Elsevier in New Biotechnology
- Vol. 93, 351-361
Open AccessSubstrate biochemical composition does not impact hydrogen consumption rate but metabolite production during batch in-situ biomethanation process
- Open Access
- 13 February 2026
- Published by Elsevier in Journal of Environmental Management
- Vol. 401, 128966
Coupling computational fluid dynamics and kinetic models using a compartmental model applied to a full-scale agricultural digester
- 13 February 2026
- Published by Elsevier in Journal of Environmental Management
- Vol. 401, 128966
Open AccessCoupling computational fluid dynamics and kinetic models using a compartmental model applied to a full-scale agricultural digester
- Open Access
- 25 January 2026
- Published by MDPI AG in Applied Sciences
- Vol. 16 (3) , 1231
Modeling and Optimization of Phenolic Compound Adsorption from Olive Wastewater Using XAD-4 Resin, Activated Carbon, and Chitosan Biosorbent
This study proposes a circular economy strategy to recover phenolic compounds by valorizing shrimp shell waste into a chitosan biosorbent (CH-B). Its adsorption efficiency was evaluated compared to commercial activated carbon (AC) and synthetic XAD-4 resin. Kinetic analysis revealed that while both pseudo-first-order (PFO) and pseudo-second-order (PSO) models exhibited high correlations (R2 0.96), both CH-B and XAD-4 resin were best described by the PFO model. This aligns with diffusion-controlled processes consistent with the porous and physical nature of these adsorbents. In contrast, AC followed the PSO model. Isotherm modeling indicated that CH-B and AC fit the Temkin model, reflecting heterogeneous surfaces, whereas XAD-4 followed the Langmuir model (monolayer adsorption). Notably, CH-B exhibited a maximum adsorption capacity (qm) of 229.2 mg/g, significantly outperforming XAD-4 (104.8 mg/g) and AC (90.2 mg/g). Thermodynamic and kinetic modeling confirmed that the adsorption mechanism was governed by a combination of electrostatic interactions, π–π stacking, and hydrogen bonding between the hydroxyl/amine groups of chitosan and phenolic compounds. Optimization using Box–Behnken design for CH-B showed optimal acidic pH and moderate temperature but non-significant effect of CH-B dose in the experimental domain. Optimisation results showed unexpected high removal efficiency at low CH-B dosages. A tentative explanation may be adsorbent aggre-gation, which needs to be confirmed by further experimental evidence.- 25 January 2026
- Published by MDPI AG in Applied Sciences
- Vol. 16 (3) , 1231
Open AccessModeling and Optimization of Phenolic Compound Adsorption from Olive Wastewater Using XAD-4 Resin, Activated Carbon, and Chitosan Biosorbent
This study proposes a circular economy strategy to recover phenolic compounds by valorizing shrimp shell waste into a chitosan biosorbent (CH-B). Its adsorption efficiency was evaluated compared to commercial activated carbon (AC) and synthetic XAD-4 resin. Kinetic analysis revealed that while both pseudo-first-order (PFO) and pseudo-second-order (PSO) models exhibited high correlations (R2 0.96), both CH-B and XAD-4 resin were best described by the PFO model. This aligns with diffusion-controlled processes consistent with the porous and physical nature of these adsorbents. In contrast, AC followed the PSO model. Isotherm modeling indicated that CH-B and AC fit the Temkin model, reflecting heterogeneous surfaces, whereas XAD-4 followed the Langmuir model (monolayer adsorption). Notably, CH-B exhibited a maximum adsorption capacity (qm) of 229.2 mg/g, significantly outperforming XAD-4 (104.8 mg/g) and AC (90.2 mg/g). Thermodynamic and kinetic modeling confirmed that the adsorption mechanism was governed by a combination of electrostatic interactions, π–π stacking, and hydrogen bonding between the hydroxyl/amine groups of chitosan and phenolic compounds. Optimization using Box–Behnken design for CH-B showed optimal acidic pH and moderate temperature but non-significant effect of CH-B dose in the experimental domain. Optimisation results showed unexpected high removal efficiency at low CH-B dosages. A tentative explanation may be adsorbent aggre-gation, which needs to be confirmed by further experimental evidence. - Open Access
Combined Continuous Resin Adsorption and Anaerobic Digestion of Olive Mill Wastewater for Polyphenol and Energy Recovery
Olive mill wastewater (OMWW) has high energetic potential due to its organic load, but its complex composition and toxicity limit efficient energy recovery. This study proposes an innovative integrated process combining continuous resin adsorption with anaerobic digestion to detoxify OMWW and recover renewable energy simultaneously. It studies the recovery of polyphenols, methane production, and substrate degradation efficiency using resin column bed heights (C1: 5.7 cm, C2: 12.1 cm, C3: 18.5 cm), as well as kinetic modeling of organic matter degradation. Adsorption reduced chemical oxygen demand (COD) by up to 80% and polyphenols by up to 64%, which significantly improved substrate biodegradability from 34% to 82%, corresponding to a methane yield of 287 mL CH4/g COD. Organic matter was fractioned into rapid (S1), moderate (S2), and slow (S3) biodegradable fractions. The highest degradation kinetics was C3, with methane production rates of K1 = 23.86, K2 = 2.47, and K3 = 2.92 mL CH4/d. However, this condition produced the lowest volumetric methane production due to excessive COD removal, including readily biodegradable matter. These results highlight the importance of optimizing the adsorption step in order to find to a balance between detoxification and energy recovery from OMWW, thus supporting the principles of circular economy and promoting renewable energy production.
Open AccessCombined Continuous Resin Adsorption and Anaerobic Digestion of Olive Mill Wastewater for Polyphenol and Energy Recovery
Olive mill wastewater (OMWW) has high energetic potential due to its organic load, but its complex composition and toxicity limit efficient energy recovery. This study proposes an innovative integrated process combining continuous resin adsorption with anaerobic digestion to detoxify OMWW and recover renewable energy simultaneously. It studies the recovery of polyphenols, methane production, and substrate degradation efficiency using resin column bed heights (C1: 5.7 cm, C2: 12.1 cm, C3: 18.5 cm), as well as kinetic modeling of organic matter degradation. Adsorption reduced chemical oxygen demand (COD) by up to 80% and polyphenols by up to 64%, which significantly improved substrate biodegradability from 34% to 82%, corresponding to a methane yield of 287 mL CH4/g COD. Organic matter was fractioned into rapid (S1), moderate (S2), and slow (S3) biodegradable fractions. The highest degradation kinetics was C3, with methane production rates of K1 = 23.86, K2 = 2.47, and K3 = 2.92 mL CH4/d. However, this condition produced the lowest volumetric methane production due to excessive COD removal, including readily biodegradable matter. These results highlight the importance of optimizing the adsorption step in order to find to a balance between detoxification and energy recovery from OMWW, thus supporting the principles of circular economy and promoting renewable energy production.
- 9 May 2025
- Published by Elsevier in Waste Management
- Vol. 203, 114869
Physicochemical properties of carbon-based materials enhance in situ biomethanation performances under organic overload
- 9 May 2025
- Published by Elsevier in Waste Management
- Vol. 203, 114869
Physicochemical properties of carbon-based materials enhance in situ biomethanation performances under organic overload
- 8 April 2025
- Published by Elsevier in Bioresource Technology
- Vol. 429, 132494
Microbial adaptation to H2 improves the conversion of volatile fatty acids to methane during in situ biomethanation even in CO2-depleted conditions
- 8 April 2025
- Published by Elsevier in Bioresource Technology
- Vol. 429, 132494
Microbial adaptation to H2 improves the conversion of volatile fatty acids to methane during in situ biomethanation even in CO2-depleted conditions
- Open Access
- 19 March 2025
- Published by Elsevier in Waste Management
- Vol. 200, 114739
Modelling anaerobic digestion of agricultural waste: From lab to full scale
- 19 March 2025
- Published by Elsevier in Waste Management
- Vol. 200, 114739
Open AccessModelling anaerobic digestion of agricultural waste: From lab to full scale
- Open Access
Integration of Digestate-Derived Biochar into the Anaerobic Digestion Process through Circular Economic and Environmental Approaches—A Review
The growing energy consumption and the need for a circular economy have driven considerable interest in the anaerobic digestion (AD) of organic waste, offering potential solutions through biogas and digestate production. AD processes not only have the capability to reduce greenhouse gas emissions but also contribute to the production of renewable methane. This comprehensive review aims to consolidate prior research on AD involving different feedstocks. The principles of AD are explored and discussed, including both chemical and biological pathways and the microorganisms involved at each stage. Additionally, key variables influencing system performance, such as temperature, pH, and C/N ratio are also discussed. Various pretreatment strategies applied to enhance biogas generation from organic waste in AD are also reviewed. Furthermore, this review examines the conversion of generated digestate into biochar through pyrolysis and its utilization to improve AD performance. The addition of biochar has demonstrated its efficacy in enhancing metabolic processes, microorganisms (activity and community), and buffering capacity, facilitating Direct Interspecies Electron Transfer (DIET), and boosting CH4 production. Biochar also exhibits the ability to capture undesirable components, including CO2, H2S, NH3, and siloxanes. The integration of digestate-derived biochar into the circular economy framework emerges as a vital role in closing the material flow loop. Additionally, the review discusses the environmental benefits derived from coupling AD with pyrolysis processes, drawing on life cycle assessment investigations. Techno-economic assessment (TEA) studies of the integrated processes are also discussed, with an acknowledgment of the need for further TEA to validate the viability of integrating the biochar industry. Furthermore, this survey examines the techno-economic and environmental impacts of biochar production itself and its potential application in AD for biogas generation, aiming to establish a more cost-effective and sustainable integrated system.
Open AccessIntegration of Digestate-Derived Biochar into the Anaerobic Digestion Process through Circular Economic and Environmental Approaches—A Review
The growing energy consumption and the need for a circular economy have driven considerable interest in the anaerobic digestion (AD) of organic waste, offering potential solutions through biogas and digestate production. AD processes not only have the capability to reduce greenhouse gas emissions but also contribute to the production of renewable methane. This comprehensive review aims to consolidate prior research on AD involving different feedstocks. The principles of AD are explored and discussed, including both chemical and biological pathways and the microorganisms involved at each stage. Additionally, key variables influencing system performance, such as temperature, pH, and C/N ratio are also discussed. Various pretreatment strategies applied to enhance biogas generation from organic waste in AD are also reviewed. Furthermore, this review examines the conversion of generated digestate into biochar through pyrolysis and its utilization to improve AD performance. The addition of biochar has demonstrated its efficacy in enhancing metabolic processes, microorganisms (activity and community), and buffering capacity, facilitating Direct Interspecies Electron Transfer (DIET), and boosting CH4 production. Biochar also exhibits the ability to capture undesirable components, including CO2, H2S, NH3, and siloxanes. The integration of digestate-derived biochar into the circular economy framework emerges as a vital role in closing the material flow loop. Additionally, the review discusses the environmental benefits derived from coupling AD with pyrolysis processes, drawing on life cycle assessment investigations. Techno-economic assessment (TEA) studies of the integrated processes are also discussed, with an acknowledgment of the need for further TEA to validate the viability of integrating the biochar industry. Furthermore, this survey examines the techno-economic and environmental impacts of biochar production itself and its potential application in AD for biogas generation, aiming to establish a more cost-effective and sustainable integrated system.
- Open Access
- 10 July 2024
- Published by Elsevier in Bioresource Technology
- Vol. 407, 131101
Improved organic matter biodegradation through pulsed H2 injections during in situ biomethanation
- 10 July 2024
- Published by Elsevier in Bioresource Technology
- Vol. 407, 131101
Open AccessImproved organic matter biodegradation through pulsed H2 injections during in situ biomethanation